Journal
CHEMICAL ENGINEERING & TECHNOLOGY
Volume 28, Issue 1, Pages 53-60Publisher
WILEY-V C H VERLAG GMBH
DOI: 10.1002/ceat.200407034
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Hydrodynamic and mass transfer characteristics such as liquid velocity, gas holdup and gas-liquid volumetric mass transfer coefficient in the riser and downcomer of the gas-liquid-solid three-phase internal loop airlift reactors with manometer solid particles were investigated. A mathematical model for the description of flow behavior and gas-liquid mass transfer of those reactors was also developed. The predicted results of this model agreed well with the experimental data.
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